散装液体危化品浮式码头金属软管失效原因分析及对策

介绍了金属软管在码头装卸船管路系统中的作用,并结合散装液体危化品浮式码头的实际,深入探讨了码头金属软管的失效原因,并提出了相应的防范措施,对提升金属软管的安全服役水平具有借鉴意义。     

非潮汐淹水对白骨壤膜脂过氧化系统的影响

通过室内模拟非潮汐淹水,探索不同淹水水位条件下,红树植物白骨壤(A.marina(Forsk.)Vierh).超氧化物歧化酶(SOD)、过氧化氢酶(CAT)、丙二醛(MDA)随时间的变化情况。结果表明,经历第二个淹水周期后,较第一个周期各梯度,白骨壤超氧化物歧化酶活性(SOD)从高到低排序不变,过氧化氢酶活性(CAT)、丙二醛的量(MDA)也表现出相同的规律。本研究结论为红树植物在人工非潮汐生境下,红树林造林的关键技术之一——淹水水位的控制提供了数据参考。     

地下水环境影响评价导则执行过程中遇到的问题及建议

对中国各地区地下水的水质情况进行了调查,分析了地下水环境管理和保护工作中的问题,指出地下水污染防治工作的重要性、迫切性。对《环境影响评价技术导则地下水环境》(HJ 610-2011)的工作等级划分、环境影响识别、环境现状调查、影响评价及污染防治等内容进行了简要介绍,汇总了评价导则执行后,对各类项目进行地下水评价过程中遇到的困难和问题,并在对各种问题进行分析的基础上,提出了有针对性的解决方法和建议。     

天然藻类吸附重金属的研究

传统的重金属废水处理技术存在耗能高、运行成本高及存在二次污染的问题等诸多劣势;而天然海藻由于其来源广、产量大,在处理重金属废水方面存在较多的优点。介绍了藻类处理重金属离子的研究背景、现状,阐述了藻类处理重金属的优点、机理,重点介绍了海藻处理废水过程中的各种影响因素,并对海藻处理废水的应用前景进行了展望。     

工业用煤气燃烧装置二氧化硫减排方式的讨论

工业用煤气是工业生产中普遍采用的气体燃料,煤气燃烧过程会产生二氧化硫,减少煤气燃烧过程的二氧化硫排放可采用煤气脱硫和烟气脱硫两种方式。本文通过对煤气脱硫工艺及烟气脱硫工艺原理及参数进行对比的方式,讨论工业用燃气燃烧装置的两种二氧化硫减排方式的优缺点,为该类装置脱硫设计提供参考。     

液体危化品在码头装卸过程中的静电危害及对策

介绍了液体危化品的特点,对装卸船作业过程中静电产生的途径及主要危害进行了分析,并提出了相应的防范对策.     

辛醇异丁醛装置化工异味综合治理

分析了辛醇异丁醛装置化工异味来源,介绍了通过技术改造、回收利用、生物除臭等方法消除化工异味的成功经验,对目前存在的问题,提出改进建议。     

基于大型乙烯成套装置工艺安全的变更管理

介绍了工艺安全变更管理的概念及相关标准法规,结合国内变更管理的现状,提出了大型乙烯成套装置工艺安全变更管理建议。     

Catalytic oxidation of CO over Pt/Fe3O4 catalysts: Tuning O2 activation and CO adsorption

• Strong metal-support interaction exists on Pt/Fe₃O₄ catalysts. • Pt metal particles facilitate the formation of oxygen vacancies on Fe₃O₄. • Fe₃O₄ supports enhance the strength of CO adsorption on Pt metal particles. The self-inhibition behavior due to CO poisoning on Pt metal particles strongly impairs the performance of CO oxidation. It is an effective method to use reducible metal oxides for supporting Pt metal particles to avoid self-inhibition and to improve catalytic performance. In this work, we used in situ reductions of chloroplatinic acid on commercial Fe₃O₄ powder to prepare heterogeneous-structured Pt/Fe₃O₄ catalysts in the solution of ethylene glycol. The heterogeneous Pt/Fe₃O₄ catalysts achieved a better catalytic performance of CO oxidation compared with the Fe₃O₄ powder. The temperatures of 50% and 90% CO conversion were achieved above 260°C and 290°C at Pt/Fe₃O₄, respectively. However, they are accomplished on Fe₃O₄ at temperatures higher than 310°C. XRD, XPS, and H₂-TPR results confirmed that the metallic Pt atoms have a strong synergistic interaction with the Fe₃O₄ supports. TGA results and transient DRIFTS results proved that the Pt metal particles facilitate the release of lattice oxygen and the formation of oxygen vacancies on Fe₃O₄. The combined results of O₂-TPD and DRIFTS indicated that the activation step of oxygen molecules at surface oxygen vacancies could potentially be the rate-determining step of the catalytic CO oxidation at Pt/Fe₃O₄ catalysts. The reaction pathway involves a Pt-assisted Mars-van Krevelen (MvK) mechanism.     

A quantitative water resource planning and management model for an industrial park level

This paper introduces an integrated water management model at the industrial park level. It suggests four approaches to water management: first, direct water reuse among users; second, water reuse among users by blending with freshwater; third, water reuse between users and a wastewater treatment plant; and fourth, groundwater recharge by reclaimed wastewater or other feasible applications in order to optimize the overall water efficiency. The model results in a comprehensive management methodology for optimizing water resources within an industrial park, seeking potential water reuse among industries, and incorporating the size and cost of reclaimed wastewater delivery systems. A case study is employed to test the model’s feasibility. An economic analysis of the optimized water use network is also carried out, showing the potential water and cost savings.